Bimodal neodymium-catalyzed polybutadiene
AssigneeLANXESS Deutschland GmbH
InventorsHeike Kloppenburg, Thomas Gross
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Abstract
The invention relates to a high molecular weight bimodal neodymium-catalysed polybutadiene having a high proportion, >95%, of cis-1,4 units and a low proportion, <1%, of 1,2-vinyl content, wherein the polybutadiene has a linear polymeric main fraction and a long chain branched polymeric fraction, wherein the slope in the RGM relationship is >0.5 for the polymeric main fraction and <0.3 for the long chain branched polymeric fraction.
Claims13
High molecular weight bimodal neodymium-catalysed polybutadiene having a high proportion, >95%, of cis-1,4 units and a low proportion, <1%, of 1,2-vinyl content, characterized in that the polybutadiene has a linear polymeric main fraction and a long chain branched polymeric fraction, wherein the slope in the RGM relationship is >0.5 for the polymeric main fraction and <0.3 for the long chain branched polymeric fraction.
Process for producing bimodal neodymium-catalysed polybutadienes according to any preceding claim, comprising the steps of:
- 1) modified catalyst production with preforming using catalyst systems based on neodymium consisting of
- component A:
- an alkoxide, a phosphonate, phosphinate and/or phosphate, a carboxylate, a complexed compound of rare earth metals with diketones and/or an addition compound of the halides of the rare earth metals with an oxygen or nitrogen donor compound, preferably neodymium versatate,
- component B:
- a dialkylaluminium hydride, preferably diisobutylaluminium hydride (DIBAH),
- component C:
- a diene, preferably butadiene or isoprene, and
- component D:
- and at least one organometallic halide, preferably ethylaluminium sesquichloride (EASC),
- wherein initially, in a first step, the components A, B and C are mixed at a temperature of −20° C. to 80° C., preferably 0° C. to 40° C., for a period of 5 minutes to 10 hours, preferably 10 minutes to 2 hours, and then the mixture is cooled down to below −10° C., preferably to below −30° C., prior to addition of component D;
- 2) optionally preforming the modified catalyst system at a temperature of −30° C. to 80° C., preferably 5° C. to 50° C., for the duration of 10 minutes to 250 hours, preferably 20 minutes to 100 hours;
- 3) polymerizing the monomers at a temperature between −20 and 100° C.,
- 4) subsequently maintaining the polymerization solution at the end, viz, at a conversion of ≧85% by weight, preferably ≧90% by weight and more preferably ≧95% by weight, of butadiene at a temperature of ≧100° C., preferably 100° C. to 140° C. and more preferably 100° C. to 125° C. for 10 to 120 min, preferably for 15 to 60 min.
Dependencies are inferred from the claim text.